Carbon nanotubes for fuel cells, method for manufacturing the same, and fuel cell using the same

ABSTRACT

Carbon nanotubes for use in a fuel cell, a method for fabricating the same, and a fuel cell using the carbon nanotubes for its electrode are provided. The internal and external walls of the carbon nanotubes are doped with nano-sized metallic catalyst particles uniformly to a degree of 0.3-5 mg/cm 2 . The carbon nanotubes are grown over a carbon substrate using chemical vapor deposition or plasma enhanced chemical vapor deposition. Since the carbon nanotubes have a large specific surface area, and metallic catalyst particles are uniformly distributed over the internal and external walls thereof, the reaction efficiency in an electrode becomes maximal when the carbon nanotubes are used for the electrode of a fuel cell. The carbon nanotubes fabricated using the method can be applied to form a large electrode. The carbon nanotubes grown over the carbon substrate can be readily applied to an electrode of a fuel cell, providing economical advantages and simplifying the overall electrode manufacturing process. A fuel cell using as the carbon nanotubes for its electrode provides improved performance.

BACKGROUND OF THE INVENTION

This application claims priority from Korean Patent Application No.2002-44631, filed on Jul. 29, 2002, in the Korean Intellectual PropertyOffice, the disclosure of which is incorporated herein in its entiretyby reference.

1. Field of the Invention

The present invention relates to carbon nanotubes, and moreparticularly, to carbon nanotubes for fuel cells, which are directlygrown over a carbon substrate and whose internal and external walls areuniformly doped with metallic catalyst particles, and a method forfabricating the carbon nanotubes, and a fuel cell using the carbonnanotubes for an electrode.

2. Description of the Related Art

Recently, with growing concerns about the environment and the exhaustionof energy resources, and the commercialization of fuel cell automobiles,there is an urgent need for the development of reliable,high-performance fuel cells that are operatable at an ambienttemperature with high energy efficiency and for the development ofpolymer membranes capable of increasing the efficiency of fuel cells.

Fuel cells are new power generating systems that convert energy producedthrough the electrochemical reactions of fuel and oxidative gas directlyinto electric energy. Such fuel cells can be categorized into fuel cellswith molten carbonate salt, which are operable at a high temperature of500-700° C., fuel cells with phosphoric acid, which are operable around200° C., alkaline electrolyte fuel cells operable between roomtemperature and 100° C., and solid polymer electrolyte (SPE) fuel cellsoperable at a temperature of ambient ˜100° C.

SPE fuel cells include proton-exchange membrane fuel cells (PEMFCs)using hydrogen gas as a fuel source and direct methanol fuel cells(DMFCs) which generate power using liquid methanol solution directlyapplied to the anode as a fuel source.

SPE fuel cells, which are emerging as the next generation of a cleanenergy source alternative to fossil fuels, have high power density andhigh-energy conversion efficiency. In addition, SPE fuel cells areworkable at an ambient temperature and are easy to hermetically seal andminiaturize, so they can be extensively applied to the fields ofpollution-free vehicles, power generating systems for house use, mobiletelecommunications equipment, medical equipment, military equipment,equipment in space, and the like.

The basic structure of a PEMFC as a power generator producing a directcurrent through the electrochemical reaction of hydrogen and oxygen isshown in FIG. 1. Referring to FIG. 1, a PEMFC has a proton-exchangemembrane 11 interposed between an anode and a cathode. Theproton-exchange membrane 11 is formed of an SPE with a thickness of50-200 μm. The anode and cathode includes anode and cathode backinglayers 14 and 15, respectively, for supplying reaction gases or liquid,and catalyst layers 12 and 13, respectively, where oxidation/reductionof reaction occur, forming catalyst electrodes (hereinafter, the anodeand cathode will be referred to as “catalyst electrodes”). In FIG. 1,reference numeral 16 denotes a carbon sheet having gas injection holesand acting as a current collector.

As hydrogen as a reaction gas is supplied to a PEMFC having thestructure as described above, hydrogen molecules decompose into protonsand electrons through oxidation reaction in the anode. These protonsreach the cathode through the proton-exchange membrane 11. Meanwhile, inthe cathode, oxygen molecules take electrons from the anode and arereduced to oxygen ions through reaction. These oxygen ions react withthe protons from the anode to produce water.

As shown in FIG. 1, in the gas diffusion electrodes of the PEMFC, thecatalyst layers 12 and 13 are formed on the anode and cathode backinglayers 14 and 15, respectively. The anode and cathode backing layers 14and 15 are formed of carbon cloth or carbon paper. The surfaces of theanode and cathode backing layers 14 and 15 are treated for reactiongases and water to easily permeate into the proton-exchange membrane 11before and after reaction.

DMFCs have a similar structure to the PEMFC described above, but useliquid methanol solution instead of hydrogen as a fuel source. Asmethanol solution is supplied to the anode, an oxidation reaction occursin the presence of a catalyst to generate protons, electrons, and carbondioxide. Although DMFCs has lower energy efficiency than PEMFCs, the useof a liquid fuel in DMFCs makes their application to portable electronicdevices easier.

Electrodes, fuel, electrolyte membranes for high energy density, highpower fuel cells have been actively researched. In addition, there havebeen attempts to increase the activity of a catalyst used in theelectrodes. Since the activity of catalysts is proportional to thereaction surface area thereof, it is necessary to increase the reactionsurface area by reducing the diameter of catalyst particles to a fewnanometers and to uniformly distribute such nano-sized catalystparticles over the electrodes.

Conventionally, catalysts such as platinum have been applied as paste,uniformly to electrode backing layers of porous carbon substrate.However, the dispersion of the catalyst in the electrode backing layersis not uniform, and the surface area of the carbon carrier andelectrical conductivity are not large enough.

Japanese Laid-open Publication No. 2000-63112 discloses a method formanufacturing single-walled carbon nanotubes into which trace of metalis incorporated by CO₂ laser irradiation of a metal containing carbonsource. In this method, the use of laser limits the area where carbonnanotubes are grown. To be applied to fuel cells, an additional step ofcoating electrodes with a paste of the carbon nanotubes is required,which makes the overall fuel cell manufacturing process complicated.

SUMMARY OF THE INVENTION

The present invention provides carbon nanotubes directly grown over acarbon substrate and whose internal and external walls are uniformlydoped with catalyst particles of a diameter of a few nanometers or less.

The present invention also provides a method for fabricating the abovecarbon nanotubes grown over the carbon substrate.

The present invention also provides a fuel cell with improvedefficiency, which is formed using the above carbon nanotubes grown overthe carbon substrate for an electrode.

According to an aspect of the present invention, there is providedcarbon nanotubes grown over a carbon substrate and whose internal andexternal walls are doped with nano-sized metallic catalyst particlesuniformly to a degree of 0.3˜5 mg/cm².

According to another aspect of the present invention, there is provideda method for fabricating carbon nanotubes grown over a carbon substrate,comprising: uniformly distributing metallic catalyst particles over thecarbon substrate; and supplying a carbon source gas at a constant rateunder atmospheric pressure and reacting the carbon source gas with themetallic catalyst particles at a temperature of 400-900 for 1-120minutes to grow carbon nanotubes over the carbon substrate.

According to still another aspect of the present invention, there isprovided a fuel cell using the above carbon nanotubes grown over acarbon substrate for an electrode.

BRIEF DESCRIPTION OF THE DRAWINGS

The above and other features and advantages of the present inventionwill become more apparent by describing in detail exemplary embodimentsthereof with reference to the attached drawings in which:

FIG. 1 shows the configuration of a fuel cell;

FIG. 2 is a scanning electron microscopic (SEM) photograph showing theuniform distribution of metallic carbon particles over a carbonsubstrate;

FIG. 3 is a SEM photograph of carbon nanotubes for use in fuel cellsaccording to the present invention;

FIG. 4 is a transmission electron microscopic (TEM) photograph of abranched carbon nanotube for use in fuel cells according to the presentinvention.

FIG. 5 shows a reaction system used in a method for fabricating carbonnanotubes according to the present invention; and

FIG. 6 illustrates., step by step, a method for fabricating carbonnanotubes according to the present invention, in which (a) illustratesuniformly distributing catalyst particles over a carbon substrate, (b)illustrates directly growing carbon nanotubes over the carbon substratewith the catalyst particles serving as seeds for the growth of thecarbon nanotubes, (c) illustrates adjusting the density of growingcarbon nanotubes, and (d) illustrates adjusting the growth of carbonnanotubes to form branched carbon nanotubes.

DETAILED DESCRIPTION OF THE INVENTION

A feature of the present invention lies in that carbon nanotubes aredirectly grown over a carbon substrate. Accordingly, the carbonsubstrate over which the carbon nanotubes according to the presentinvention are grown can be readily applied to a fuel cell. Moreover,according to the present inventions rather than growing upright, carbonnanotubes branch off while growing over the carbon substrate, therebyincreasing a reaction surface area thereof. The internal or externalwalls of the carbon nanotubes are uniformly doped with mono, binary,ternary or higher catalytic particles, preferably selected from thegroup consisting of Pt, Ru, Fe, and Co, having a diameter of a fewnanometers. Therefore, when such carbon nanotubes according to thepresent invention are used in a fuel cell, the reaction efficiency in anelectrode of the fuel call becomes maximal. Also, according to thepresent invention, as the carbon nanotubes grow, the metallic catalystparticles are evenly distributed along the internal and outer walls ofthe carbon nanotubes and fixed stably thereto so as not to be affectedby an external force.

FIG. 3 is a scanning electron microscopic (SEM) photograph of carbonnanotubes according to the present invention. As is apparent in FIG. 3,the carbon nanotubes according to the present invention are grownbranched, not upright, so that their surface area becomes large.

FIG. 4 is a transmission electron microscopic (TEM) photograph of abranched carbon nanotube according to the present invention. In FIG. 4,numerous metallic catalyst particles are uniformly distributed on theinternal and external walls of the carbon nanotube, wherein metalliccatalyst particles adsorbed onto the external wall are illustrated asblack dots, and metallic catalyst particles adsorbed onto the internalwall are illustrated as gray dots. According to the present invention,it is preferable that the degree of dispersion of the metallic catalystparticles be in the range of 0.3-5 mg/cm². If the metallic catalystparticles have a degree of dispersion of less than the lower limit, thereaction activity of the metallic catalyst particles is insufficient. Ifthe metallic catalyst particles have a degree of dispersion of greaterthan the upper limit, they tend to lump together and inhibit carbonnanotube growth.

A method for fabricating carbon nanotubes for catalyst support inaccording to the present invention will be described step by step withreference to FIG. 6. In a method for fabricating carbon nanotubesaccording to the present invention, after uniformly dispersing metalliccatalyst particles over a carbon substrate, as illustrated in (a) ofFIG. 6, carbon source gas is supplied at a constant rate underatmospheric pressure and reacted at 400-900 for 1-120 minutes to growcarbon nanotubes over the carbon substrate, as illustrated in (b) ofFIG. 6. When the carbon nanotubes grow to some extent, as illustrated in(c) of FIG. 6, hydrogen gas or ammonia gas may be applied to fabricatebranched carbon nanotubes, as illustrated in (d) of FIG. 6. While carbonnanotubes grow, most metallic catalyst particles adsorb onto theinternal and external walls of the carbon nanotubes. However, somemetallic catalyst particles may act as nuclei from which the carbonnanotubes branch off when subjected to etching using reducing gas, suchas hydrogen gas or ammonia gas. Therefore, the branched carbon nanotubesaccording to the present invention can be fabricated. In particular,hydrogen gas converts metallic catalyst particles in oxidized form intoreduced form, thereby increasing the activity of the catalyst particlesand leading to the growth of branched carbon nanotubes. Alternatively,branched carbon nanotubes may be fabricated by appropriately adjustingthe flow rate of carbon source gas and reaction temperature and timesuch that metallic carbon nanotubes can migrate along the growing carbonnanotubes.

In the method for fabricating carbon nanotubes for use in a fuel cellaccording to the present invention, uniformly dispersing the metalliccatalyst particles over the carbon substrate may be achieved byelectrophoresis, thermal spraying, sputtering, chemical vapor deposition(CVD), and any other techniques common to one of ordinary skill in theart.

FIG. 5 shows a reaction system used in a method for fabricating carbonnanotubes according to the present invention. A bare carbon substrate 4is inserted into a slit of a quartz boat 5. The quartz boat 5 in whichthe bare carbon substrate 5 is mounted is placed at the center of areactor 2. In FIG. 5, reference numeral 3 denotes a heating unit. Afterargon gas or nitrogen gas is supplied into the quartz tube underatmospheric pressure, carbon source gas is supplied at a constant rateunder atmospheric pressure and reacted at 400-900 for 1-120 minutes togrow carbon nanotubes over the carbon substrate. Suitable carbon sourcegas that can be used in the present invention may be any gas commonlyused by one of ordinary skill in the art, in which preferred carbonsource gas includes ethylene, carbon monoxide, carbon dioxide, andmethane. If the reaction temperature is less than 400, carbon particles,rather than nanotubes, result. If the reaction temperature is above 900,the activity of the metallic carbon particles is reduced, and the growthrate of carbon nanotubes greatly drops. It is preferable that the carbonsource gas is supplied at a rate of 10-1000 sccm. If the flow rate ofthe carbon source gas is less than 10 sccm, the amount of carbon sourcegas is insufficient to grow carbon nanotubes. If the carbon source gasis supplied at a rate of 1000 sccm, undesirable carbon particles adhereto the grown carbon nanotubes because of the supply of excess carbonsource gas.

As described above, according to the present invention, carbon nanotubesare grown over a carbon substrate. Such a carbon substrate may be carboncloth or carbon paper. The carbon substrate over which the carbonnanotubes have been grown according to the present invention can bereadily applied as an electrode of a fuel cell, thereby simplifying theoverall process for manufacturing electrodes of fuel cells. Inconventional electrode manufacturing processes, a paste of catalysts ora paste of catalysts and carbon nanotubes is applied to electrodebacking layers, such as carbon cloth. In other words, conventionalelectrode manufacturing processes are complicated because they involveseparate steps for processing electrode substrates, doping the electrodesubstrate with catalysts, and forming complete electrodes. However,according to the present invention, while carbon nanotubes are directlygrown over a carbon substrate that can be used for an electrode,catalytic particles are uniformly distributed over the growing carbonnanotubes. As a result, the electrode manufacturing process is markedlysimplified, thereby lowering the cost of products.

In a method for fabricating carbon nanotubes for use in fuel cellsaccording to the present invention, plasma enhanced chemical vapordeposition (PECVD) instead of common CVD may be applied. In PECVD, whilecarbon source gas is supplied between two electrodes of a reactor wheremetallic catalysts are previously placed, microwaves or radio waves areapplied to the reactor to activate the carbon source gas into a plasmastate and to grow carbon nanotubes over the electrodes by the activatedenergy. “Plasma” collectively refers to gaseous ions generated whengaseous molecules are bombarded with high-energy free electronsgenerated by glow discharging and the free electrons.

Fuel cells can be classified into alkaline fuel cells, phosphoric acidfuel cells, molten carbonate salt fuel cells, solid oxide fuel cells,and solid polymer electrolyte (SPE) fuel cells according to the kinds ofelectrolytes. Alkaline fuel cells, phosphoric acid fuel cells, and SPEfuel cells require platinum catalysts. Branched carbon nanotubesdirectly grown over a carbon substrate according to the presentinvention can be applied as electrodes in alkaline fuel cells,phosphoric acid fuel cells and SPM fuel cells (PEMFC and DMFC).

The present invention will be described in greater detail with referenceto the following examples. The following examples are for illustrativepurposes and are not intended to limit the scope of the invention.

EXAMPLE 1

Platinum (Pt) as a metallic catalyst was dispersed over a water-proofedcarbon paper serving as a carbon substrate for 1 minute byelectrophoresis, and a uniform dispersion of the Pt particles wasconfirmed using scanning electron microscope (SEM)-energy dispersivespectroscopy (EDS). The result is shown in FIG. 2. The carbon substrateover which the Pt particles had been uniformly distributed was mountedin a quartz boat and placed at the center of a reactor. The reactor waspurged with argon gas at 5000 sccm under atmospheric pressure while thetemperature of the reactor was elevated to 500. When the temperature ofthe reactor reached 500, acetylene was supplied into the reactor as acarbon source gas at 10 sccm under atmospheric pressure for 60 minute tosynthesize carbon nanotubes. Next, while argon gas was supplied into thereactor at 300 sccm under atmospheric pressure, the temperature of thecarbon nanotubes were dropped to room temperature to provide carbonnanbtubes doped with the Pt particles uniformly to a degree of 1 mg/cm².

EXAMPLE 2

Carbon nanotubes were synthesized in the same manner as in Example 1,except that Fe₂O₃ instead of Pt was used as the catalyst. As a result,carbon nanotubes doped with Fe particles uniformly to a degree of 2mg/cm² were obtained.

EXAMPLE 3

Branched carbon nanotubes were synthesized in the same manner as inExample 1, except that, after 10 minutes from the supply of the carbonsource gas to allow carbon nanotubes to grow to some extent, hydrogengas was supplied into the reactor at 50 sccm for 20 minutes. As aresult, branched carbon nanotubes doped with the catalyst particlesuniformly to a degree of 2 mg/cm² were obtained.

As described above, carbon nanotubes whose internal and external wallsare uniformly doped with metallic catalyst particles having a diameterof a few nanometers according to the present invention, which aredirectly grown over a carbon substrate, have a wide specific surfacearea, especially when the carbon nanotubes are branched off, so that thecarbon nanotubes according to the present invention maximize thereaction efficiency in an electrode when used for the electrode of afuel cell. In addition, since the carbon nanotubes are directly grownover a carbon substrate that can be used for an electrode, the carbonsubstrate with the carbon nanotubes grown thereover can be readilyapplied as an electrode of a fuel cell at low costs, without the needfor complicated electrode manufacturing processes. Moreover, since mono,binary, ternary or higher metallic elements can be used as a catalyst,the carbon nanotubes grown over a carbon substrate according to thepresent invention can be used for cathodes as well as anodes. Whenbranched carbon nanotubes are grown over a carbon substrate using CVD orPECVD in q method according to the present invention, the branchedcarbon nanotubes grown over the carbon substrate have a larger surfacearea, so that they can be used for more effective electrodes. A fuelcell using as an electrode a carbon substrate over which the carbonnanotubes according to the present invention are grown provides improvedperformance, compared to conventional fuel cells.

While the present invention has been particularly shown and describedwith reference to exemplary embodiments thereof, it will be understoodby those of ordinary skill in the art that various changes in form anddetails may be made therein without departing from the spirit and scopeof the present invention as defined by the following claims.

1. A method for fabricating carbon nanotubes, the method comprising: (a)uniformly distributing metallic catalyst particles over a carbonsubstrate; and (b) supplying a carbon source gas at a constant rateunder atmospheric pressure and reacting the carbon source gas with themetallic catalyst particles at a temperature of 400-900° C. for 1-120minutes.
 2. The method of claim 1, wherein the carbon source gas isethylene, carbon monoxide, carbon dioxide, or methane.
 3. The method ofclaim 1, wherein step (a) of uniformly distributing metallic catalystparticles over the carbon substrate is performed by electrophoresis,thermal spraying, sputtering, or chemical vapor deposition.
 4. Themethod of claim 1, wherein step (b) further comprises applyingmicrowaves or radio waves to activate the carbon source gas into plasmastate.
 5. The method of claim 1, wherein step (b) further comprisesadjusting reaction conditions such that the growing carbon nanotubesbranch off.
 6. The method of claim 5, wherein adjusting the reactionconditions comprises supplying a reducing gas after about 10 minutesfrom the supplying of the carbon source gas.
 7. The method of claim 6,wherein the reducing gas is hydrogen gas or ammonia gas.
 8. The methodof claim 5, wherein adjusting the reaction conditions comprisesadjusting the flow rate of the carbon source gas and reactiontemperature and time.